US20120039830A1 - Process for producing powdery composition and powdery cosmetic - Google Patents

Process for producing powdery composition and powdery cosmetic Download PDF

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Publication number
US20120039830A1
US20120039830A1 US13/255,266 US201013255266A US2012039830A1 US 20120039830 A1 US20120039830 A1 US 20120039830A1 US 201013255266 A US201013255266 A US 201013255266A US 2012039830 A1 US2012039830 A1 US 2012039830A1
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Prior art keywords
powdery
powdery composition
slurry
amount
producing
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Inventor
Takuma Kurahashi
Hideo Hata
Yoshito Ogura
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Shiseido Co Ltd
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Shiseido Co Ltd
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Assigned to SHISEIDO COMPANY LTD. reassignment SHISEIDO COMPANY LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HATA, HIDEO, KURAHASHI, TAKUMA, OGURA, YOSHITO
Publication of US20120039830A1 publication Critical patent/US20120039830A1/en
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    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00—Cosmetics or similar toiletry preparations
    • A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/72—Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds
    • A61K8/84—Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds obtained by reactions otherwise than those involving only carbon-carbon unsaturated bonds
    • A61K8/89—Polysiloxanes
    • A61K8/896—Polysiloxanes containing atoms other than silicon, carbon, oxygen and hydrogen, e.g. dimethicone copolyol phosphate
    • A61K8/898—Polysiloxanes containing atoms other than silicon, carbon, oxygen and hydrogen, e.g. dimethicone copolyol phosphate containing nitrogen, e.g. amodimethicone, trimethyl silyl amodimethicone or dimethicone propyl PG-betaine
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00—Cosmetics or similar toiletry preparations
    • A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/19—Cosmetics or similar toiletry preparations characterised by the composition containing inorganic ingredients
    • A61K8/25—Silicon; Compounds thereof
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00—Cosmetics or similar toiletry preparations
    • A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
    • A61K8/33—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing oxygen
    • A61K8/37—Esters of carboxylic acids
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00—Cosmetics or similar toiletry preparations
    • A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
    • A61K8/49—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing heterocyclic compounds
    • A61K8/4993—Derivatives containing from 2 to 10 oxyalkylene groups
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
    • A61Q1/00—Make-up preparations; Body powders; Preparations for removing make-up
    • A61Q1/12—Face or body powders for grooming, adorning or absorbing

Definitions

  • FIG. 1 is a diagrammatic representation of FIG. 1 .
  • the present invention relates to a method for producing a powdery composition, a powdery cosmetic material prepared by incorporating the powdery composition obtained by the production method, and a method for producing a solid powdery cosmetic material using the powdery composition obtained by the production method. More particularly, the present invention relates to a method for producing a powdery makeup product such as a foundation or a makeup base, which has an excellent feeling of use and provides excellent long-lasting makeup.
  • the powdery cosmetic material obtained according to the production method is such that while the feeling of use when applied on the skin has a moist feeling like a liquid, a satisfactory texture of being soft dry and uniform is obtained.
  • the powder is uniformly coated with the oily component by slurring mixing in a volatile solvent, after the cosmetic material is applied, the cosmetic material is likely to be blended in with the sebum secreted from the skin, and the cosmetic material is not sufficiently satisfactory in terms of long-lasting makeup. Therefore, even though the cosmetic material can be provided as a powdery cosmetic material for autumn and winter seasons, it has been found difficult to apply the cosmetic material to a powdery cosmetic material for spring and summer seasons.
  • the production method described above has a problem that when a powder which undergoes a large color change when wetted with an oily component is incorporated, the powdery cosmetic material becomes dark by wetting, and therefore, the skin wearing makeup turns markedly dull due to sebum. Thus, even though the powdery cosmetic material has a good feeling of use, it has been difficult to incorporate the cosmetic material in large amounts.
  • the present invention provides a method for producing a powdery composition, the method comprising:
  • a drying apparatus which performs drying of the slurry by converting the slurry into fine liquid droplets by a mechanical shear force and blowing a dry gas to the fine liquid droplets
  • the non-volatile oily component contains:
  • a lipophilic nonionic surfactant in an amount of 0.1% to 2% by mass relative to the total amount of the powdery composition.
  • the present invention provides a method for producing a powdery composition such as described above, wherein the drying apparatus used in the drying step is a drying apparatus including:
  • a shearing means that shears the slurry by a shearing member provided inside the housing and converts the slurry into fine liquid droplets
  • a supplying means that supplies the slurry to the shearing member in the housing
  • a blowing means that blows a dry gas into the housing, and supplying the drying gas to the slurry that has been converted to fine liquid droplets by the shearing means to bring the dry gas and the fine liquid droplets into contact;
  • a collecting means that collects a powdery composition produced by drying the slurry.
  • the present invention provides a method for producing a powdery composition such as described above wherein in the slurry preparation step, the slurry is obtained by mixing the powder component and the non-volatile oily component in the volatile solvent using a medium agitating mill, and cracking and/or pulverizing and/or dispersing the powder component.
  • the powder component is contained in an amount of 70% to 98% by mass, and preferably 80% to 95% by mass, relative to the total amount of the powdery composition
  • the non-volatile oily component is contained in an amount of 2% to 30% by mass, and preferably 5% to 20% by mass, relative to the total amount of the powdery composition.
  • the powder component further contains an extender pigment, a white pigment, and a color pigment.
  • the present invention provides a powdery cosmetic material containing the powdery composition obtained by the production method described above, in an amount of 80% to 100% relative to the total amount of the powdery cosmetic material.
  • the present invention also provides a method for producing a solid powdery cosmetic material, including a solidification step of filling the powdery composition obtained by any one of the production methods in a container, optionally together with other optional components such as a pearl pigment, and solidifying the powdery composition and the optional components by dry press molding, and a solid powdery cosmetic material obtainable by the production method.
  • a powdery composition in which the powdery component does not aggregate even in the drying step, and the powdery component is uniformly coated with the non-volatile oily component and is imparted with water-repellent and oil-repellent effects, can be obtained.
  • a powdery cosmetic material which has an excellent feeling of use, particularly, excellent adhesion to the skin, and an excellent moist feeling, and provides excellent long-lasting makeup, can be provided.
  • a solid powdery cosmetic material which can be very easily applied, and has an excellent feeling of use, and provides excellent long-lasting makeup, can be obtained.
  • FIG. 1 is a schematic configuration diagram of the apparatus used in an embodiment of the present invention.
  • FIG. 2 is a diagram showing an example of the medium agitating mill in a secitional view.
  • FIG. 3 is a diagram showing an example of the medium agitating mill in a sectional view.
  • the present invention relates to a method for producing a powdery composition, which includes a slurry preparation step of mixing a powder component and a non-volatile oily component in a volatile solvent to obtain a slurry, and a particular drying step of obtaining the powder composition with the volatile solvent removed from the slurry.
  • the inventors of the present invention particularly paid attention to a step of removing a volatile solvent in a so-called wet production method, by which a powdery composition is produced from a slurry containing a volatile solvent, and conducted a thorough investigation on various drying processes.
  • the inventors of the present invention have conducted a thorough investigation on such problems, and as a result, they found that when a drying apparatus which has a shearing mechanism of converting a slurry into fine liquid droplets, and is capable of drying the slurry in the form of fine liquid droplets is used, the resulting powdery composition is finely divided so that cracking with a dry pulverizing machine is not needed.
  • the inventors also found that at the time of preparing a slurry to be provided for such drying, when a powder component and a non-volatile oil component containing a particular amino-modified silicone are used to prepare a slurry in a volatile solvent, a powdery cosmetic material which is excellent in terms of smoothness when applied on the skin, uniform finish, and spreadability, has excellent adhesion to the skin and an excellent fit feeling, and provides an excellent long-lasting makeup effect, is obtained. Furthermore, the inventors found that when a lipophilic nonionic surfactant is incorporated into the oily component, the powdery cosmetic material has a superior moist feeling.
  • FIG. 1 is a diagram showing an example of the configuration of the apparatus used in the production method of the present invention.
  • the production method of the present invention includes a slurry preparation step of mixing a powder component and a non-volatile oily component in a volatile solvent to obtain a slurry, and a drying step of drying the slurry to remove the volatile solvent, and obtaining a powdery composition.
  • a slurry is obtained by mixing the powder component and the non-volatile oily component in the volatile solvent using the medium agitating mill 10 shown in FIG. 1 and cracking, pulverizing and dispersing the powder component (slurry preparation step).
  • the slurry thus obtained is temporarily collected in a storage tank 12 , and is supplied to a drying apparatus 14 (drying step) at a predetermined flow rate.
  • the drying apparatus 14 used in the present embodiment performs drying of the slurry by converting the slurry into fine liquid droplets through a mechanical shear force, that is, a shear force generated by the rotation of shearing members (plate-shaped members 34 a , 34 b and 34 c ) provided in a shearing means 18 , and blowing a dry gas to the fine liquid droplets.
  • a mechanical shear force that is, a shear force generated by the rotation of shearing members (plate-shaped members 34 a , 34 b and 34 c ) provided in a shearing means 18 , and blowing a dry gas to the fine liquid droplets.
  • the shape of the shearing members may have any shape such as a blade shape or a disc shape, in addition to the plate shape such as described above.
  • a powdery composition is produced using a drying apparatus 14 which performs drying of the slurry in the form of fine liquid droplets, a powdery composition can be obtained almost without the occurrence of aggregation of the powder component at the time of drying. Accordingly, it is possible to provide a powdery cosmetic material having an excellent feeling of use when applied on the skin. Also, because it is not necessary to carry out cracking again after drying, the production of the powdery composition is also excellent in terms of productivity and work environment properties.
  • the solid powdery cosmetic material thus obtained not only has an excellent feeling of use, but also has excellent usage properties such as easy appliability with a puff.
  • a medium agitating mill 10 in order to mix the essential components to be incorporated in a volatile solvent.
  • a medium agitating mill When a medium agitating mill is used, a slurry in which the powder component is coated on the surface with the non-volatile oily component appropriately uniformly to the extent that will not affect the long-lasting makeup effect, can be obtained.
  • a powdery cosmetic material which has a superior feeling of use and superior usage properties can be obtained.
  • a powdery cosmetic material containing a pearl pigment when produced, first, a slurry is prepared using a powder component except for the pearl pigment in the slurry preparation step, and this slurry is dried in the drying step to obtain a powdery composition which does not contain the pearl pigment. Then, the powdery composition which does not contain the pearl pigment is mixed with the pearl pigment, and a powdery cosmetic material is suitably obtained using this powder mixture.
  • a powdery cosmetic material which is excellent in terms of product quality, such as smoothness, a feeling of fit to the skin, uniform finish, a moist feeling, and good spreadability, and in terms of productivity and work environment properties, and also has an excellent pearl-like texture.
  • a Henschel mixer registered trademark
  • (C) A method of adding a certain specific powder component having strong aggregability, such as an elastic polymer powder or a fine particle powder, into a volatile solvent, preliminarily mixing this powder component with the solvent with a disper-mixer or the like as necessary, subsequently cracking, pulverizing and dispersing the mixture using a medium agitating mill to obtain a dispersion liquid, adding another powder component or a non-volatile oily component to the dispersion liquid, and further processing the mixture using a wet mixing machine or a medium agitating mill.
  • a certain specific powder component having strong aggregability such as an elastic polymer powder or a fine particle powder
  • a medium agitating mill is a device which accommodates a dispersion liquid formed from a powder component (and a non-volatile oily component) and a solvent in a vessel containing a solid dispersing medium (medium) such as beads, and agitating the liquid in the vessel to perform cracking, pulverization and dispersion of the powder component by means of an impact force, a frictional force or the like exerted by the medium.
  • a medium agitating mill is a device which accommodates a dispersion liquid formed from a powder component (and a non-volatile oily component) and a solvent in a vessel containing a solid dispersing medium (medium) such as beads, and agitating the liquid in the vessel to perform cracking, pulverization and dispersion of the powder component by means of an impact force, a frictional force or the like exerted by the medium.
  • FIG. 2 and FIG. 3 are schematic configuration diagrams respectively showing examples of the medium agitating mill that is suitably used in the present invention.
  • the medium agitating mills that can be suitably used in the present invention are not limited to these, and any medium agitating mill may be used as long as it is capable of achieving the object of the present invention.
  • the medium agitating mill 110 shown in FIG. 2 as an example includes an generally cylindrical-shaped vessel 112 , a drive shaft 114 inserted through the vessel 112 , a drive motor 116 which rotationally drives the drive shaft 114 , and plural sheets of agitating discs 118 a to 118 f that are fitted to the drive shaft.
  • the inside of the vessel 112 is divided into a dispersing chamber 120 which performs cracking, pulverization and dispersion of the powder component, and a extraction chamber 122 which extracts the processed dispersion liquid.
  • the dispersing chamber 120 of the vessel 112 is provided with a supply port 124 for supplying a dispersion liquid to be processed, and the extraction chamber 122 is provided with a extraction port 126 for extracting the processed dispersion liquid.
  • a partition wall 130 provided with an opening 128 is provided between the dispersing chamber 120 and the extraction chamber 122 , and near this partition wall 130 , a separating disc 132 fitted to the drive shaft 114 is disposed to cover the opening 128 of the partition wall 130 .
  • a gap is provided between the partition wall 130 and the separating disc 132 , and this gap is used as a separating slit 134 which separates the solid dispersing medium from the dispersion liquid to be processed.
  • the dispersion liquid containing the powder component, the non-volatile oily component, and the volatile solvent (hereinafter, simply referred to as solvent) is successively supplied through the supply port 124 to the dispersing chamber 120 inside the vessel 112 , and the dispersion liquid in the dispersing chamber 120 moves successively in the direction of the extraction chamber 122 .
  • the drive shaft 114 is rotationally driven by the drive motor 116 , and the agitating discs 118 a to 118 f are rotating.
  • the dispersing chamber 120 is filled with a large number of solid dispersing media 136 , and the solid dispersing media 136 are agitated together with the dispersion liquid by the rotation of the agitating discs 118 a to 118 f .
  • the aggregated powder component in the dispersion liquid is cracked, pulverized and dispersed by the impact force, shear stress or the like exerted by the solid dispersing media 136 .
  • the separating slit 134 has a size that will prevent the solid dispersing media 136 from escaping from the dispersing chamber 120 to the extraction chamber 122 .
  • the separating slit separates the dispersion liquid (powder component+solvent) from the solid dispersing media 136 , so that only the dispersion liquid enters the extraction chamber.
  • FIG. 3 is a schematic configuration diagram of an annular type medium agitating mill.
  • the medium agitating mill 210 of FIG. 3 includes a vessel 212 which has an generally W-shaped cross-section that is symmetric about the central axis A, a rotor 214 which is generally inversely U-shaped and is capable of rotating around the central axis A, and a drive motor 216 that rotationally drives the rotor 214 .
  • a circular space 218 is formed between the inner surface of the vessel 216 and the outer surface of the rotor 214 , and this circular space 218 has a shape having an generally V-shaped cross-section which lies on both sides of the central axis A.
  • a supply port 220 for sending the dispersion liquid (powder component+solvent) to be processed to the circular space 218 , and a extraction port 222 for extracting the dispersion liquid to be processed from the circular space 218 are formed in the vessel 212 .
  • the circular space 218 is filled with solid dispersing media 224 , so that the circular space 218 is used as a dispersing chamber that performs cracking, pulverization and dispersion of the powder component in the dispersion liquid.
  • the dispersion liquid supplied from the supply port 220 is transported to the circular space 218 via an inlet slit 226 .
  • the dispersion liquid thus transported moves inside the circular space 218 and is extracted through the extraction port 222 via an outlet slit 228 .
  • the dispersion liquid and the solid dispersion media 224 inside the circular space 218 are agitated by rotating the rotor 214 about the central axis A within the circular space 218 .
  • the aggregated powder component in the dispersion liquid is cracked, pulverized and dispersed by the impact force, shear stress or the like exerted from the solid dispersing media 224 .
  • the dispersion liquid passes through the outlet slit 228 and is extracted from the extraction port 222 .
  • the outlet slit 228 has a size that will prevent the solid dispersing media 224 from escaping from the circular space 218 , and functions as a separating means that separates the dispersion liquid (powder component+solvent) from the solid dispersing media 224 . Furthermore, the rotor 214 is provided with a returning hole 230 for returning the solid dispersing media 224 to the inlet side, so that the solid dispersing media 224 are kept from staying in the vicinity of the outlet.
  • the reason for cracking, pulverizing and dispersing a powder component and a non-volatile oily component in a volatile solvent using a medium agitating mill is that since the mixed and dispersed state of the powder component and the non-volatile oily component can be enhanced, and the surface of the powder component can be coated with the non-volatile oily component appropriately uniformly to the extent that will not affect the long-lasting makeup effect, a powdery cosmetic material having a good feeling of use can be obtained. Furthermore, a powder having strong aggregability can be easily cracked and uniformly dispersed in a volatile solvent.
  • medium agitating mill examples include batch type bead mills such as a basket mill; horizontal type, vertical type, and annular type continuous bead mills; sand grinder mills; ball mills; Micros (registered trademark) and the like.
  • batch type bead mills such as a basket mill; horizontal type, vertical type, and annular type continuous bead mills; sand grinder mills; ball mills; Micros (registered trademark) and the like.
  • suitable examples include batch type bead mills such as a basket mill; horizontal type, vertical type, and annular type continuous bead mills; sand grinder mills; ball mills; Micros (registered trademark) and the like.
  • the medium agitating mill there are no particular limitations on the medium agitating mill as long as the medium agitating mill adequate for the purpose.
  • any medium agitating mill which, when a powder component which is in an aggregated state is incorporated, can resolve the aggregation of the powder component to agitate and disperse the powder component to a state close to primary particles, and can appropriately uniformly coat the powder surfaces with a non-volatile oily component to the extent that will not affect the long-lasting makeup effect, can be used without any particular limitations.
  • the media to be used in the medium agitating mill are preferably beads, and beads produced from raw materials such as glass, alumina, zirconia, steel and flint may be used, while beads made of zirconia are particularly preferred.
  • beads having a diameter of about 0.5 to 10 mm are used with preference, but in the present invention, beads having a diameter of approximately 2 mm to 5 mm are used with preference. If the size of the bead diameter is too small, cracking of the extender pigments such as mica and talc proceeds excessively, and an adverse effect is exerted on the feeling of use, or the hardness after molding is increased so that appliability is deteriorated, or caking or the like is easily induced. On the other hand, if the size of the bead is too large, aggregation of the powder component cannot be sufficiently resolved, and uniform coating with a non-volatile oily component becomes difficult.
  • the powder component and the non-volatile oily component that are mixed in the slurry preparation step will be described below. Furthermore, components that can be incorporated into the powder cosmetic material in addition to the essential components in the slurry preparation step will also be described below.
  • volatile solvent that is used to mix the incorporated components of the powder cosmetic material
  • examples of the volatile solvent include purified water, cyclic silicones, ethanol, light liquid isoparaffin, lower alcohols, ethers, LPG, fluorocarbons, N-methylpyrrolidone, fluoroalcohols, volatile linear silicones, and next generation Freon.
  • Representative examples of the lower alcohols include ethanol and isopropanol.
  • the amount of the volatile solvent that is used in the slurry preparation step cannot be specified because the amount depends on the polarity, specific gravity and the like of the volatile solvent used, but in the case of using a medium agitating mill, it is important to secure fluidity that enables the process.
  • the drying apparatus used in the production method of the present invention is not limited to that in FIG. 1 , and any drying apparatus equipped with a shearing means which mechanically converts a slurry into fine liquid droplets is acceptable.
  • the drying apparatus 14 in FIG. 1 is not limited to that in FIG. 1 , and any drying apparatus equipped with a shearing means which mechanically converts a slurry into fine liquid droplets is acceptable.
  • a hollow-shaped housing 16 which serves as the site for performing drying of the slurry; a shearing means 18 which converts a slurry into fine liquid droplets by means of rotating shearing members (plate-shaped members 34 a , 34 b , and 34 c ) that are provided inside the housing 16 ; a supplying means 20 which supplies the slurry to the shearing members (plate-shaped members 34 a , 34 b and 34 c ) inside the housing 16 ; a blowing means 22 which blows a dry gas into the housing 16 , and supplies the dry gas to the slurry that has been converted to fine liquid droplets by the shearing means 18 ; and a collecting means 24 which collects a powdery composition generated by drying the slurry.
  • the housing 16 has a generally cylindrical shape which is vertical and hollow, and is provided at the upper part with an emission port 26 which emits the powdery composition and the dry gas, and is provided at the lower part with a blowing port 28 which supplies the dry gas from the blowing means 22 into the housing 16 . Also, a supply port 30 which supplies the slurry into the housing 16 is disposed between the emission port 26 located at the upper part of the housing 16 and the blowing port 28 located at the lower part.
  • the shearing means 18 includes a rotating shaft 32 that is installed in the direction perpendicular to the bottom of the housing 16 , shearing members (plate-shaped members 34 a , 34 b and 34 c ) that are provided at a right angle to the rotating shaft 32 , and a drive means 36 for rotating the rotating shaft 32 .
  • the drive means 36 is disposed outside the housing 16 , and transfers a rotating force to the shearing members (plate-shaped members 34 a , 34 b and 34 c ) through the rotating shaft 32 .
  • the shearing members shown in FIG. 1 are constituted by three plate-shaped members 34 a , 34 b and 34 c that are provided at a right angle to the rotating shaft 32 at intervals in the vertical direction.
  • shearing members are located in the lower part of the supply port 30 for the slurry and in the upper part of the blowing port 28 for the dry gas.
  • the plate-shaped members 34 a , 34 b and 34 c rotate in the horizontal direction about the rotating shaft 32 inside the housing 16 , and this mechanical shear force causes the conversion of the slurry into fine liquid droplets.
  • the supply means 20 supplies the slurry sent from the storage tank 12 into the housing 16 .
  • the slurry supplied to the housing 16 drops toward the plate-shaped members 34 a , 34 b and 34 c , and is converted into fine liquid droplets by the rotating plate-shaped members 34 a , 34 b and 34 c .
  • the dry gas sent from the blowing means 22 is blown into the housing 16 through the blowing port 28 .
  • the dry gas is supplied toward the tangential direction of the horizontal cross-section of the housing 16 , and since the plate-shaped members 34 a , 34 b and 34 c are in a rotating movement, the dry gas stream blown into the housing 16 is changed to a swirling flow.
  • the slurry in the form of fine liquid droplets When the slurry in the form of fine liquid droplets is brought into contact with this dry gas stream, the slurry is further micronized and is dried to form a powdery composition.
  • This powdery composition is blown up together with the dry gas stream to the upper part of the housing 16 , and is emitted through the emission port 26 .
  • the powdery composition emitted out of the housing 16 through the emission port 26 is collected by a collection means 24 .
  • a classification means 38 is provided in the area of the emission port 26 inside the housing 16 .
  • the classification means 38 is constructed as an orifice provided at the emission port 26 , and prevents large grains, lumps, undried materials and the like from entering the collection means 24 .
  • the configuration of the classification means is not limited to this, and any other configuration may be used.
  • a powdery composition with less aggregation can be obtained.
  • the reason why a powdery composition with less aggregation is obtained is speculated to be that when the slurry is converted to fine liquid droplets, the amount of the powder component present in the liquid droplets is small, and therefore, aggregation at the time of drying does not easily occur, that the aggregation of the powder component occurring during the drying process is resolved by the shear force exerted by the shearing members or the swirling flow, and the like.
  • shearing members constituted of plate-shaped members that rotate in the horizontal direction have been described herein, but in addition to this, shearing members constituted of plate-shaped members that rotate in the vertical direction (the rotating shaft extending in the horizontal direction) may also be provided.
  • the shape of the shearing member is not limited to the shape described above, and for example, a blade shape (a cutter provided perpendicularly to the tip of a rod-shaped member which is attached perpendicularly to the rotating shaft, or the like), a disc shape and the like may be used. Also, there are no particular limitations on the number of the shearing members, or the like.
  • the drying apparatus described above is of a type called flash dryer, and examples thereof include a Spin Flash Dryer manufactured by APV Nordic Anhyro A/S, a Drymeister manufactured by Hosokawa Micron Corp., and a vertical agitation dryer manufactured by Tsukishima Kikai Co., Ltd.
  • a Spin Flash Dryer manufactured by APV Nordic Anhyro A/S a Drymeister manufactured by Hosokawa Micron Corp.
  • a vertical agitation dryer manufactured by Tsukishima Kikai Co., Ltd.
  • any of vertical type and horizontal type drying apparatuses may be used as long as the apparatus has a shearing mechanism in the system.
  • the temperature of the dry gas used at the time of drying can be varied depending on the boiling point of the volatile solvent used. Also, since the drying efficiency increases as the temperature of the dry gas is higher, it is desirable to set the temperature of the dry gas high, to the extent that there are no adverse effects such as heat-induced alteration of the constituent components of the powdery composition.
  • the apparatus acquires excellent explosion proofness, and therefore, the work environment properties are also improved.
  • recovery of the solvent is also made possible by adopting a solvent recovery mechanism such as a condenser.
  • the production method further includes a solidification step of filling the powdery composition in a container and solidifying the powdery composition by dry molding.
  • a solidification step of filling the powdery composition in a container and solidifying the powdery composition by dry molding As the method for solidification, conventionally known dry press molding and the like may be used.
  • a solid powdery cosmetic material thus obtained exhibits an excellent feeling of use that is equivalent to or superior than the solid powdery cosmetic materials produced by wet methods, and also has an advantage of good usage properties (appliability with a puff), which is an advantage of dry molding.
  • a powdery cosmetic material containing an added pearl pigment representative examples of which include titanated mica, glass pearl and the like
  • a medium agitating mill it is preferable to first obtain a powdery composition using the portion of the powder component excluding the pearl pigment, by subjecting the powder component to the slurry preparation step and the drying step described above.
  • This powdery composition and a necessary amount of a pearl pigment are mixed in a dry mixing machine which exerts a weak shear force, such as a Henschel mixer or a Nauta mixer, to obtain a mixed powder, and this mixed powder is filled in a container and is further subjected to dry molding to obtain a powdery cosmetic material.
  • the powdery cosmetic material obtained by this method is excellent in terms of the feeling of use, usage properties, and the long-lasting makeup effect, and also has an excellent pearl-like texture.
  • pearl pigment there are no particular limitations on the pearl pigment, and those pearl pigments that are generally used as conventional cosmetic materials can be used.
  • Representative examples thereof include titanated mica, iron oxide-coated titanated mica, lower-order titanium oxide-coated titanated mica, photochromic titanated mica, and pigments which use talc, glass, synthetic fluorphlogopite, silica, bismuth oxychloride and the like instead of mica as substrate.
  • examples of the coating material include, in addition to titanium oxide, lower-order titanium oxide, iron oxide, alumina, silica, zirconia, zinc oxide, cobalt oxide, aluminum and the like.
  • functional pearl pigments having excellent optical properties include pearl pigments coated on the surfaces with resin particles (JP-A No.
  • pearl pigments coated on the surfaces with aluminum hydroxide particles JP-A No. 2002-146238
  • pearl pigments coated on the surfaces with zinc oxide particles JP-A No. 2003-261421
  • pearl pigments coated on the surfaces with barium sulfate particles JP-A No. 2003-61229) and the like.
  • These functional pearl pigments having the pearl pigment surfaces coated with various particles are such that when a strong force is exerted on the particles that are coating the surfaces, the particles tend to easily fall off.
  • a force is exerted on the pearl pigment only at the time of mixing with the powdery composition, and therefore, it is not necessary to mix the pigment with the powdery composition with such a strong force, and the particles coating the pearl pigments are less likely to fall off. Therefore, according to the production method described above, a functional pearl pigment can be incorporated into the powdery cosmetic material without impairing the function of the pearl pigment.
  • the amount of incorporation of the pearl pigment is preferably 0% to 20% by mass relative to the total amount of the powdery cosmetic material.
  • the amount of incorporation of the powdery composition obtained by the production method of the present invention into the cosmetic material is preferably 80% to 100% by mass, and more preferably 90% to 100% by mass, relative to the total amount of the powdery cosmetic material. If a pearl pigment is not incorporated, the powdery composition may be incorporated at a proportion of 100%.
  • the powdery composition obtained by the production method of the present invention has the non-volatile oily component as a binder and the powder component sufficiently mixed and pulverized, and aggregation occurs less during drying. Therefore, a subsequent pulverization step is not needed, and a solid powdery cosmetic material can be easily produced by directly dry press molding the powdery composition, without adding a non-volatile oily component as an additional binder. Furthermore, when the powdery composition is produced, without press molding, into a powdery cosmetic material such as loose powder, the powdery composition may be directly filled in a container and prepared as a final product.
  • powdery compositions respectively having different compositions may be prepared, and those powdery compositions may be mixed to adjust the color or the like for use.
  • the powdery composition obtained by the production method of the present invention are suitably applied to powdery cosmetic materials or solid powdery cosmetic materials, such as foundation, eye shadow, rouge, body powder, powdered perfume, baby powder, pressed powder, deodorant powder, and face powder.
  • the powdery composition when used as a solid powdery cosmetic material, the powdery composition exhibits an effect of improving the feeling of use or the long-lasting makeup effect.
  • the powder that can be incorporated as the powder component used in the slurry preparation step and the drying step of the present invention is not particularly limited, as long as the powder can be used as a cosmetic material. Furthermore, a powder which has been hydrophobized in advance may also be used. According to the production method of the present invention, when a particular amino-modified silicone is contained in the non-volatile oily component, water-repellent and oil-repellent effects can be imparted to the powder. Therefore, even if a powder which has not been hydrophobized in advance is used, a powdery cosmetic material having an excellent long-lasting makeup effect can be obtained.
  • Specific components of the powder include an extender pigment, a white pigment, a color pigment, a spherical powder and the like.
  • plural different powder components such as an extender pigment, a white pigment, and a color pigment can be simultaneously incorporated.
  • Examples of the extender pigment include talc, kaolin, sericite, muscovite, phlogopite, lepidolite, biotite, calcined talc, calcined sericite, calcined muscovite, calcined phlogopite, vermiculite, magnesium carbonate, calcium carbonate, aluminum silicate, barium silicate, calcium silicate, magnesium silicate, strontium silicate, tungstic acid metal salts, magnesium, silica, zeolite, barium sulfate, calcined calcium sulfate (calcined gypsum), calcium phosphate, fluorapatite, ceramic powder, metal soaps (for example, zinc myristate, calcium palmitate, and aluminum stearate), and red synthetic fluorphlogopite containing iron atoms in the crystal structure.
  • the red synthetic fluorphlogopite containing iron atoms in the crystal structure is known as a cosmetic raw material which can impart a vivid color tone and a transparent texture, and has a high quality feeling of use (JP-A No. 6-9210, and JP-A No. 11-279432).
  • JP-A No. 6-9210, and JP-A No. 11-279432 JP-A No. 6-9210, and JP-A No. 11-279432
  • it is a raw material which undergoes significant dulling of color when wetted with a non-volatile oily component or sebum, and it has been difficult to incorporate the material in large amounts in the conventional art.
  • dulling of color can be mitigated.
  • the amount is preferably 2% to 20% by mass relative to the total amount of the powdery composition after dried. If the amount is less than 2% by mass, there is a possibility that the effect of high quality feeling of use of the red synthetic fluorphlogopite can be hardly expected. On the other hand, if the amount is greater than 20% by mass, there is a possibility that the color change caused by sebum is increased, and the long-lasting makeup effect may be decreased, which is not preferable.
  • white pigment examples include boron nitride, titanium dioxide, zinc oxide, photochromic titanium oxide (titanium dioxide sintered with iron oxide), and reduced zinc oxide.
  • the color pigment examples include inorganic red pigments (for example, iron oxide (red iron oxide), and iron titanate), inorganic brown pigments (for example, y-iron oxide), inorganic yellow pigments (for example, yellow iron oxide and yellow clay), inorganic black pigments (for example, black iron oxide and lower-order titanium oxide), inorganic violet pigments (for example, mango violet and cobalt violet), inorganic green pigments (for example, chromium oxide, chromium hydroxide, and cobalt titanate), inorganic blue pigments (for example, ultramarine blue and Prussian blue), organic pigments such as barium or aluminum lakes (for example, organic pigments such as Red No. 201, Red No. 202, Red No. 204, Red No.
  • inorganic red pigments for example, iron oxide (red iron oxide), and iron titanate
  • inorganic brown pigments for example, y-iron oxide
  • inorganic yellow pigments for example, yellow iron oxide and yellow clay
  • inorganic black pigments for example
  • Red No. 220 Red No. 226, Red No. 228, Red No. 405, Orange No. 203, Orange No. 204, Yellow No. 205, Yellow No. 401, and Blue No. 404; Red No. 3, Red No. 104, Red No. 106, Red No. 227, Red No. 230, Red No. 401, Red No. 505, Orange No. 205, Yellow No. 4, Yellow No. 5, Yellow No. 202, Yellow No. 203, Green No. 3, and Blue No. 1), and natural coloring materials (for example, chlorophyll and ⁇ -carotene).
  • natural coloring materials for example, chlorophyll and ⁇ -carotene
  • spherical powder examples include silicone elastomer powder, silicone powder, silicone resin-coated silicone elastomer powder, polyamide resin powder (nylon powder), polyethylene powder, polymethyl methacrylate powder, polystyrene powder, powder of a copolymer resin of styrene and acrylic acid, benzoguanamine resin powder, polyurethane resin powder, and spherical silica.
  • a powder component that can be conventionally incorporated into cosmetic materials can be incorporated.
  • one kind or two or more kinds of these powder components preferably three or more kinds, and more preferably four or more kinds of powder components can be used.
  • the amount of incorporation of the powder component used in the slurry preparation step is 70% to 98% by mass, preferably 80% to 95% by mass, and more preferably 85% to 95% by mass, relative to the total amount of the powdery composition after dried. If the amount of incorporation is less than 70% by mass, there is a possibility that the water repellency and oil repellency may be insufficient. Furthermore, if the amount of incorporation is greater than 98% by mass, there is a possibility that the moist feeling may be insufficient.
  • the amount of incorporation of the powder component used in the slurry preparation step is most preferably 85% to 95% by mass relative to the total amount of the powdery composition after dried, from the viewpoint of the balance between the long-lasting makeup effect and the feeling of use such as moist feeling.
  • the non-volatile oily component contains a particular amino-modified silicone.
  • an amino-modified silicone having a functional group equivalent of 1000 to 10,000 and a viscosity at 25° C. of 200 to 2000 mm 2 /s is used.
  • the viscosity is less than 200 mm 2 /s, it is difficult to obtain a sufficient water-repellent and oil-repellent effects, and if the viscosity is greater than 2000 mm 2 /s, since the fluidity of the oily component is low at the time of drying, aggregation or non-homogenization is prone to occur, and there is a possibility that stable mass production may be hindered.
  • the functional group equivalent is less than 1000 or greater than 10,000, the water-repellent and oil-repellent effects may be insufficient.
  • an amino-modified silicone having a functional group equivalent of 1000 to 3000 and a viscosity at 25° C. of 600 to 1300 mm 2 /s is used.
  • an amino-modified silicone may be a side-chain diamine type amino-modified silicone represented by the following formula (1).
  • X, R and R′ each represent an alkyl group having 1 to 4 carbon atoms; and m and n each represent a positive number of 1 or greater, so that 1 ⁇ m+n ⁇ 1000.
  • a representative compound thereof is known as Amodimethicone (aminoethylaminopropylmethylsiloxane-dimethylsiloxane copolymer), and commercially available products include KF-8002, KF-8004, KF-880, KF-867 (all manufactured by Shin-Etsu Chemical Co., Ltd.) and the like.
  • the amount of incorporation of the amino-modified silicone used in the present invention is preferably 0.1% to 2% by mass relative to the total amount of the powdery composition after dried. If the amount of incorporation is less than 0.1% by mass, sufficient water-repellent and oil-repellent effects may not be obtained. Furthermore, if the amount of incorporation is greater than 2% by mass, water-repellent and oil-repellent effects may be obtained, but the feeling of use may be deteriorated, which is not preferable.
  • the non-volatile oily component preferably contains a lipophilic nonionic surfactant.
  • a lipophilic nonionic surfactant having an HLB value of 2 to 10, and preferably 3 to 6, can be used.
  • sorbitan fatty acid esters for example, sorbitan monooleate, sorbitan monoisostearate, sorbitan monolaurate, sorbitan monopalmitate, sorbitan monostearate, sorbitan sesquioleate, sorbitan trioleate, diglycerol sorbitan penta-2-ethylhexanoate, and diglycerol sorbitan tetra-2-ethylhexanoate); glycerin polyglycerin fatty acids (for example, mono-cottonseed oil fatty acid glycerin, glyceryl monoerucate, glyceryl sesquioleate, glyceryl monostearate, ⁇ , ⁇ ′-glyceryl oleate pyroglutamate, and glyceryl monostearate malate); propylene glycol fatty acid esters (for example, propylene glycol monostearate); hardened castor oil derivative
  • the amount of incorporation of the lipophilic nonionic surfactant is preferably 0.1% to 2% by mass relative to the total amount of the powdery composition after dried. If the amount of incorporation is less than 0.1% by mass, the effect of enhancing the moist feeling of use may not be sufficiently obtained. Furthermore, if the amount of incorporation is greater than 2% by mass, a moist feeling may be obtained, but since the powdery composition is likely to be blended with sebum, the long-lasting makeup effect may be deteriorated, which is not preferable.
  • non-volatile oily component used in the present invention include, in addition to the particular amino-modified silicone and the lipophilic nonionic surfactants, liquid fats and oils, solid fats and oils, waxes, hydrocarbons, higher fatty acids, higher alcohols, ester oils, silicone oils, oil-soluble ultraviolet absorbers such as octocrylene and octyl methoxycinnamate and the like, and there are no particular limitations as long as the oily component can be used in cosmetic materials.
  • the non-volatile oily components can be used singly or in combination of two or more kinds.
  • the non-volatile oily component can function as a binder for solid powdery cosmetic materials.
  • the amount of incorporation of the non-volatile oily component is 2% to 30% by mass, preferably 5% to 20% by mass, and more preferably 5% to 15% by mass, relative to the total amount of the powdery composition after dried. If the amount of the non-volatile oily component is too small, moldability for the solidification step, and the feeling of use such as smoothness, a feeling of fit to the skin, uniform finish, a moist feeling, and spreadability may be insufficient. On the other hand, if the amount of the oily component is too large, the feeling of use as a powdery cosmetic material, such as stickiness, may be impaired, or aggregation may occur during the drying step.
  • moisturizers such as polyhydric alcohols, sugars, and amino acids
  • water-soluble polymers such as polyhydric alcohols, sugars, and amino acids
  • ultraviolet absorbers such as polyhydric alcohols, sugars, and amino acids
  • metal ion sequestering agents such as sodium bicarbonate
  • pH adjusting agents such as sodium bicarbonate
  • skin nutrients such as sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bicarbonate, sodium bi
  • the method for evaluation of the feeling of use (good spreadability, a feeling of fit to the skin, smoothness, a moist feeling, and fine quality) and the long-lasting makeup effect over time (fading, shining, dulling of color, and powder flaking) of the powdery cosmetic material is as follows.
  • Test Example 1-1 to Test Example 1-6 having the compositions indicated in Table 1, the powder component and the non-volatile oily component were mixed in ethyl alcohol (50% by mass in outparts) using a disper-mixer, and the mixture was cracked, pulverized and dispersed using a medium agitating mill (sand grinder mill, using zirconia beads having a diameter of 2 mm ⁇ ). Thus, a slurry was obtained. Subsequently, the slurry was converted into fine liquid droplets by a mechanical shear force using a Spin Flash Dryer (manufactured by APV Nordic Anhyro A/S), and a dry gas was blown to dry the fine liquid droplets. Thus, a powdery composition was obtained. The powdery composition thus obtained was filled in a medium-sized dish, and was subjected to dry press molding by a known method. Thus, a solid powdery cosmetic material was produced.
  • a medium agitating mill sand grinder mill, using zirconia beads having
  • Test Example 1-7 the solid powdery cosmetic material was produced using a conventional, so-called dry method.
  • the powder component and the non-volatile oily component were mixed in a Henschel mixer, and then the mixture was pulverized two times with a pulverizer. Subsequently, the pulverization product was filled in a medium-sized dish, and was subjected to dry press molding by a known method. Thus, a solid powdery cosmetic material was obtained.
  • Test Example 1-7 using a conventional, so-called dry method, even if a particular amino-modified silicone was incorporated, the effect of enhancing the long-lasting makeup effect was insufficient, and the feeling of use was inferior.
  • solid powdery cosmetic materials having the compositions indicated in Table 2 were produced by fixing the amount of incorporation of the amino-modified silicone, and changing the amount of incorporation of sorbitan sesquiisostearate, which is a lipophilic nonionic surfactant.
  • the solid powdery cosmetic materials were all produced by the same process as that used in Test Example 1-1. Evaluations of the long-lasting makeup effect and the feeling of use are presented in Table 2.
  • Test Example 2-3 the effect of sorbitan sesquiisostearate of improving the usage properties was not obtained, and in Test Example 2-4, it was confirmed that although the moist feeling was enhanced, the cosmetic material was prone to be blended with sebum, and therefore, the cosmetic material lacked the long-lasting makeup effect.
  • a lipophilic nonionic surfactant was incorporated in an amount of 0.1% to 2% by mass in addition to the particular amino-modified silicone as an oily component, the long-lasting makeup effect and the moist feeling were excellent.
  • solid powdery cosmetic materials having the compositions indicated in Table 3 were produced by fixing the amounts of incorporation of the amino-modified silicone and sorbitan sesquiisostearate, and changing the amount of incorporation of red synthetic fluorphlogopite containing iron atoms in the crystal structure, and an evaluation of the feeling of use was performed.
  • the solid powdery cosmetic materials were all produced by the same process as that used in Test Example 1-1.
  • a production method which improves the product quality of powdery cosmetic materials and ameliorates the productivity for the production process can be provided.
  • a powdery cosmetic material particularly, a powdery makeup cosmetic material such as foundation, having an excellent moist feeling of use and an excellent long-lasting makeup effect (preventing makeup smudging) can be obtained.

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WO2014046883A1 (fr) * 2012-09-21 2014-03-27 Elc Management Llc Compositions cosmétiques en forme de poudre en suspension et procédés correspondants
US9370471B2 (en) 2012-09-21 2016-06-21 Elc Management Llc Slurry powder cosmetic compositions and methods
US9700493B2 (en) 2012-12-21 2017-07-11 Estee Lauder International, Inc. Slurry powder cosmetic compositions and methods
US20170216154A1 (en) * 2014-08-08 2017-08-03 Shiseido Company, Ltd. Solid powder cosmetic
US20190110967A1 (en) * 2017-10-18 2019-04-18 L'oreal Water-based cosmetic composition comprising an effect pigment and a cosmetic active
WO2024047519A1 (fr) * 2022-08-29 2024-03-07 Kaolin Group Pty Ltd Procédé de séparation par voie sèche

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JP5974160B2 (ja) * 2013-02-26 2016-08-23 株式会社日立産機システム インクジェットプリンタ用インク及び印字物
JP6114066B2 (ja) * 2013-02-28 2017-04-12 株式会社コーセー 固形粉末化粧料
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JP6603618B2 (ja) * 2016-06-02 2019-11-06 株式会社日本バリアフリー 粉体の製造方法

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JP3315160B2 (ja) 1991-09-04 2002-08-19 トピー工業株式会社 赤色合成雲母、その製法及び該雲母を含有する紫外線遮断剤
JPH1192688A (ja) 1997-09-17 1999-04-06 Shiseido Co Ltd 複合粉末
JP4141527B2 (ja) 1998-03-30 2008-08-27 株式会社資生堂 合成フッ素金雲母粉末を用いた着色剤、およびそれを配合した化粧料
JP4145496B2 (ja) 2000-08-31 2008-09-03 三好化成株式会社 新規複合粉体及びこれを配合した化粧料
JP4833452B2 (ja) 2001-08-10 2011-12-07 パナソニック電工株式会社 床用配線器具
JP3671013B2 (ja) 2002-03-07 2005-07-13 株式会社資生堂 複合粉末、それを配合したメークアップ化粧料、及び複合粉末の製造方法
JP4505211B2 (ja) * 2002-11-21 2010-07-21 東色ピグメント株式会社 表面処理粉体の製造方法、アミノ変性シリコーン処理粉体及び化粧料
JP5422092B2 (ja) * 2005-07-29 2014-02-19 株式会社 資生堂 粉末化粧料の製造方法
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WO2014046883A1 (fr) * 2012-09-21 2014-03-27 Elc Management Llc Compositions cosmétiques en forme de poudre en suspension et procédés correspondants
EP2897583A4 (fr) * 2012-09-21 2016-05-11 Elc Man Llc Compositions cosmétiques en forme de poudre en suspension et procédés correspondants
US9370471B2 (en) 2012-09-21 2016-06-21 Elc Management Llc Slurry powder cosmetic compositions and methods
US9597267B2 (en) 2012-09-21 2017-03-21 Elc Management Llc Slurry powder cosmetic compositions and methods
US9700493B2 (en) 2012-12-21 2017-07-11 Estee Lauder International, Inc. Slurry powder cosmetic compositions and methods
GB2523968B (en) * 2012-12-21 2020-04-29 Estee Lauder Int Inc Slurry powder cosmetic compositions and methods
US20170216154A1 (en) * 2014-08-08 2017-08-03 Shiseido Company, Ltd. Solid powder cosmetic
US10583070B2 (en) * 2014-08-08 2020-03-10 Shiseido Company, Ltd. Solid powder cosmetic
US20190110967A1 (en) * 2017-10-18 2019-04-18 L'oreal Water-based cosmetic composition comprising an effect pigment and a cosmetic active
US10765611B2 (en) * 2017-10-18 2020-09-08 L'oreal Water-based cosmetic composition comprising an effect pigment and a cosmetic active
WO2024047519A1 (fr) * 2022-08-29 2024-03-07 Kaolin Group Pty Ltd Procédé de séparation par voie sèche

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